利用图像处理技术在二维流化床试验装置上研究了水煤膏的混合过程。
The mixing of CWP (Coal Water Paste) in the two dimensional fluidized bed with jet was investigated by digital image processing.
除常规煤粉锅炉的自动或联锁保护装置外，根据循环流化床锅炉的特点，增加以下要求。
The following requirements are added as per the features of CFB boiler besides the automatic or interlock protection device of normal pulverized coal boiler.
氧化亚氮(N2O)是一种对大气环境有很大破坏作用的污染气体，煤的流化床燃烧是其重要来源。
Nitrous oxide (N2O) is a pollutant gas which has very strong destruction influence on atmosphere environment. Coal combustion in fluidized beds is an important resource for N2O.
循环流化床锅炉与煤粉相比，在汽水侧的控制方式上基本相同。
In the control mode of steam water side, circulating fluid bed boiler is basically the same as pulverized coal boiler.
应用离散单元方法对流化床内煤粒的运动进行了模拟。
The motions of coal particles was simulated with the Discrete Element Method in the bulling fluidized bed.
利用下行气流振动床代替流化床 ，研究了煤的碎裂特性 。
The fragmentation influences the char combustion behavior in a fluidized bed combustor.
并在一个固定床燃烧试验台上对这种复合型煤的燃烧特性进行了研究。
Experimental study was conducted of the combustion characteristics of this type of coal in a fixed-bed furnace.
在固定床光氧化反应器中，对神府煤不同密度级组分进行了紫外光光氧化研究。
The UV photooxidation characteristics of different density macerals of Shenfu coal have been studied in a fixed bed photoreactor.
现有的气流床气化技术均为高温熔渣气化技术，使国内资源丰富的双高煤无法利用。
All the existing entrained-flow gasification technologies belong to the technology of high slagging temperature process so that domestic resourceful double-high coal cant be used.
本文建立了以煤燃烧成灰为床料的循环流化床总体质量平衡数学模型。
The total mass balance of Circulating Fluidized bed Combustion (CFBC) with coal ash as bed inventory is studied.
分析了流化床煤燃烧氟析出特性，并进行了流化床石灰石燃烧固氟试验。
The fluorine emission characteristics and industrial experiment results of fluorine retention during coal combustion in fluidized bed were reported.
在以循环床锅炉循环灰为热载体、部分气化产生的半焦为锅炉燃料的煤的部分气化技术中，循环灰中的氧化钙对降低焦油产率、提高煤气产率是有利的。
Calcium oxide in circulating ash is favorable to decrease the yield of tar and increase the yield of gas in partial coal gasification process with the circulating fluidized bed technology.
从安装、运行、检修和技改的角度分析了影响燃烧劣质煤的循环流化床锅炉长周期运行的因素。
This article analysed the factors affecting long period working of the circulation fluidized bed boiler from the Angle of assembling, running, examining and repairing.
流化床催化反应过程、煤的流化床燃烧与气化等多种流化床工业应用都涉及高温操作。
The catalytic reaction process in fluidized beds, the coal combustion and gasification in the bed, and other various industrial processes all involve high temperature operation.
空气重介流化床干法选煤工艺是一项具有重大经济价值的洁净煤技术。
The dry cleaning of coal with ADMFB is a cleaning technique of coal with great economic value.
在此基础上，还就空气加入量、蒸汽加入量及加煤速率对床温、煤气组成、煤气热值、碳转化率和气化效率的影响做了预测和分析。
The effects of the feed rate of air, steam and coal on bed temperature, gas composition, calorific value, carbon conversion and gasification efficiency are predicted and analyzed with the model.
一维移动床模拟链条锅炉层状煤燃烧试验系统提供了一种重要的层状煤燃烧特性研究手段。
An important layer combustion character research method may provide by the one-dimensional moving bed simulation traveling grate stoker boiler combustion system.
在一个固定床燃烧实验台上对这种复合蜂窝煤的燃烧特性进行了研究。
Experimental study was conducted of the combustion characteristics of this type of honeycomb briquette in a fixed-bed furnace.
在流化床燃烧条件下，N2O由煤中的氮转化而来。
N2O is formed by nitrogen in coal under fluidized bed conditions.
循环流化床锅炉在启动过程中普遍存在投油量过大，开始投煤时间把握不准等现象，导致启动过程中资源过度浪费，甚至会出现启动失败的情况。
Because of over consumption of oil and inaccurate coal-feeding time in the start-up process of the circulating fluidized bed(CFB) boiler, resource waste and even the start-up failure occur.
循环流化床锅炉的烟气和烟尘性质与常规煤粉炉相比有较大差异。
There are greater differences for gas and dust characters between the circulating fluidized-bed(CFB) and normal boiler.
热等离子体煤裂解制乙炔下行床反应器工艺的严重结焦是制约该过程稳定操作与连续运行的瓶颈。
The key problem of coking seriously restricts the stable and continuous operation in thermal plasma downer reactor for the coal cracking process to produce acetylene production.
针对循环流化床锅炉的返料器、分离器和成品煤粒径等问题，介绍了国内外解决问题的经验和措施。
In view of several problems of return loop, separator and final coal grain size in CFB boilers, the improvement measure and experience were described.
针对差速循环流化床的结构及特有形式，采用小室模型的方法，对炉内煤的燃烧及其物理、化学反应过程进行了相应的仿真计算。
According to the special structure of the differential velocity bed, a simulation calculation of the coal combustion and the physical and chemical process was carried out by the cell model.
增压流化床联合循环（PFBC-CC）发电技术是一种新型的洁净煤技术。
Pressurized fluidized bed combustion combined cycle(PFBC CC) power generation is a new clean coal technology.
在不同实验条件下，用实验室规模小型电加热流化床制取不同煤质煤颗粒样品。
The electric heating fluidized bed is used to produce the varieties coal ranks of coal particles, in different experimental conditions.
煤的部分空气气化联合循环发电是一种把煤气化技术和循环流化床技术结合起来的洁净煤发电技术。
Partial gasification combined cycle generation system of coal is a clean coal technology associating coal gasification with circulation fluidized bed technology.
探讨了粉状铬铁矿在流化床内的流化性质、还原过程和加煤条件。
Investigates experimentally the fluidization and reduction processes and coal - adding conditions of powdered chromite ores in a fluidized bed.
用固定床反应器模拟合成气制备炉，对天然气与煤联合气化反应过程进行了研究。
The reaction process of natural gas and coal was investigated using a fixed-bed reactor to model the furnace for preparing synthesis gas.
研究了各煤种对常压固定床空气气化的适应性，分析了各煤种的常压固定床空气气化的气化指标。
The adaptability of all coal samples to the atmospheric fixed-bed gasification with air is studied, and gasification indexes of the atmospheric fixed-bed coal gasification with air are analyzed.
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